Background of the Invention
[0001] The present invention relates to a drain device for the removal of condensate from
systems under pressure. For example, in a gas dehydration system, the system is under
a continuous steady pressure and the gas is dehydrated continuously by means of a
process such as a pressure swing adsorption process or a membrane process or the like.
In a continuous process under pressure, any significant deviation in the pressure
reduces the efficiency of the process by a multiple factor. Thus in the dehydration
of a gas under pressure, moisture should be removed on a continuous basis without
a significant reduction in the pressure of the system or without interruption of the
continuous flow.
[0002] Many devices have been developed to drain condensate from systems used for dehydration
of a gas. Most generally these devices require interruption of the process entirely
or a variation in the system pressure which substantially reduces the efficiency of
the system.
[0003] U.S. Patents 4,116,650 and 4,400,187 to Arlo E. Lane disclose a device for eliminating
droplets of water from a stream of compressed air in which the air is passed through
a plug of porous water absorbent material which absorbs the droplets. Continued passage
of the air through the plug evaporates the water from the plug. In this situation,
compressed air is needed to effect the evaporation.
[0004] U.S. Patent 4,345,767 to Brian P. Neal utilizes the action of a piston which is deflected
upwardly to permit ejection of moisture through an aperture into which the piston
fits. This device requires the system pressure be interrupted during ejection of water.
[0005] U.S. Patent 4,874,408 to Kenneth W. Overby features a drain which is an enclosed
bowl suspended beneath a sump, and an aspiration tube which extends from within the
bowl such that air circulated into the bowl causes the liquid to be aspirated through
the tube. This device requires a change in pressure to aspirate the liquid.
[0006] In continuous gas systems, such as dehydration of gas, the moisture is ordinarily
condensed upon the moisture leaving the primary dehydration stream. Upon condensation
it is desirable to remove the liquid from the system continuously.
[0007] The present invention provides a device for continuously removing liquid condensate
from continuous systems under pressure without significant lowering of the pressure
or interruption of the system.
Summary of the Invention
[0008] The present invention provides a condensate drain device with no moving parts which
continuously removes liquid condensate from gas systems under pressure.
[0009] The condensate drain device comprises (a) a metal housing substantially cylindrical
in shape having a two-stage central longitudinal bore, an upper stage wherein the
bore is threaded internally and is larger than a lower stage wherein the bore is threaded
internally to accommodate a conduit; (b) a metal cap shaft externally threaded just
below the cap and adapted to be screwed into the upper stage bore of the housing,
the cap shaft having a two-stage central longitudinal bore wherein an upper stage
bore is internally threaded to accommodate a conduit and is larger than a lower stage
bore, the lower stage bore exiting through a shaft face, the face having cross shaped
slots; (c) a wicking disk, seated in the upper stage bore of the housing, circular
in shape with an uncompressed thickness up to about 3 mm and having a hole in the
center, the disk circumference being substantially equal to the circumference of the
interior of the upper stage bore of the housing; and
(d) a baffle disk, circular in shape residing on top of the wicking disk, the baffle
disk having a circumference slightly smaller than the circumference of the interior
of the upper stage bore of the housing and having a thickness up to about 2 mm such
that when the cap shaft is screwed into the upper stage bore of the housing, pressure
is applied by the face of the cap shaft to the metal baffle disk.
[0010] The condensate drain device functions in a very simple manner. Liquid enters the
upper stage bore of the cap shaft and travels downwardly through the cap shaft bore
to the shaft face where the liquid travels horizontally in the slots of the cap shaft
face toward the wall of the upper stage bore of the housing. The liquid then travels
downwardly in the space between the baffle disk and the upper stage bore wall to the
wicking disk below the baffle disk. The liquid then again travels horizontally by
means of wicking from the outer edge of the wicking disk to the center of the disk
where the liquid exits through the hole in the wicking disk and travels downwardly
through the lower stage bore of the housing where the liquid exits the drain device
into a conduit or other suitable receptacle means. When the liquid leaves the wicking
disk, the liquid is no longer under the positive pressure of the system.
[0011] Although the entry pressure of the gas containing the liquid condensate may be 100
psi at the entry into the drain device at the top of the bore of the cap shaft, there
is very little pressure loss through the exit of the housing lower stage bore. The
compression applied to the wicking disk by the baffle disk prevents the escape of
a significant amount of gas through the wet wicking disk while the liquid proceeds
to drain efficiently and rapidly.
Brief Description of the Drawings
[0012]
FIG. 1 is an exploded perspective view of one embodiment of the present invention;
FIG. 2 is another exploded perspective view of the same embodiment of the present invention;
and
FIG. 3 is a graph depicting dry air loss v. water removal capacity.
Detailed Description of the Invention
[0013] FIG. 1 and
FIG. 2 illustrate exploded perspective views of a condensate drain device 10. The device
10 has a metal housing 12 substantially cylindrical in shape. The housing 12 has a
two-stage central longitudinal bore 28 and 32. The upper stage bore 28 is larger than
the lower stage bore 32. Each of the stages of the bore 28 and 32 are threaded at
least part way from the exterior of the bore inwardly. The larger stage bore 28 accommodates
a cap shaft 14. The threaded portion 26 of the cap shaft 14 mates with the threaded
portion 28 of the metal housing. The cap shaft 14 preferably has a gasket 24 seated
in a notch on the lower portion of the cap shaft 14. The gasket 24 prevents seepage
of air up the cap shaft 14.
[0014] The face of the cap shaft 14 has shallow slots 20 to allow liquid to proceed from
the exit 22 of the longitudinal bore to the outside edge of the cap shaft 14. When
the cap shaft 14 is screwed into the housing 12, the slots 20 on the cap shaft face
contact a baffle disk 16. The baffle disk 16 is a hard disk, e.g., metal, plastic
or the like, and is slightly smaller than the upper stage bore 28 of the housing 12.
This allows liquid which has proceeded from the exit 22 through the slots 20 to the
edge of the disk 16 to proceed downwardly at the outside edge of the disk 16 to make
contact with the wicking disk 18.
[0015] The wicking disk 18 circumferentially fits snugly into the upper stage bore 28 of
the housing 12. The wicking disk 18 is made of a material which readily allows liquid
to wick from one portion of the disk to another. The wicking disk 18 has a hole in
the center to allow liquid to easily exit downwardly through the lower stage bore
32 to a conduit or suitable receptacle.
[0016] When the cap shaft 14 is screwed into place in the upper stage bore 28 of the housing
12, pressure is placed on the baffle disk 16 which in turn compresses the wicking
disk 18. The desired amount of pressure applied by the cap shaft 14, can be determined
by utilizing the graph depicted in
FIG. 3. For instance, if it is desired that approximately 3 ml of liquid exit the system
per minute then with the system under operating pressure, the cap shaft 14 would be
screwed into the upper stage bore 28 until a dry air loss of 1 liter of air per minute
escapes the exit from the lower stage bore 32. It is important that the pressure setting
of the cap shaft 14 be carried out when the device 10 and the wicking disk 18 are
dry and the system is under its operating pressure. Although up to 2 liters or more
of dry air per minute may escape through the exit 32 of the device 10 when the wicking
disk 18 is dry, only minuscule portions of gas escape when the system is operating
and the wicking disk 18 is wet.
[0017] The wicking disk is preferably made of a material which can be wetted by a liquid
such as water, but which is not substantially swellable nor very absorbing. Examples
include polypropylene, polyester and the like. One of the preferred materials for
use as a wick disk is a non-woven fabric. The wicking disk is up to about 3 mm thick,
preferably from about 2 to about 2.5 mm in thickness. When the wicking disk is compressed
by the pressure of the baffle disk, the thickness of the wicking disk is diminished
to about 0.4 mm.
[0018] Typical uses of the device of the present invention include systems for dehydrating
gases. For instance, in the dehydration of natural gas, one method for removing the
small amount of moisture in the gas is by use of a dehydration membrane. The membrane
is made up of hollow fibers in a module and the gas is passed through the module under
a high pressure of several hundred psi. As the gas contacts the membrane surface,
the moisture in the gas rapidly passes through the membrane thus effecting a separation
of the gas and the moisture. The moisture is then condensed to liquid form and exits
the system through the condensate drain device of this invention.
[0019] Because little or no pressure is lost when condensate exits a high pressure system
through the device of the present invention, the device of the present invention is
suitable for use in many high pressure systems wherein it is desirable to remove condensate
without interruption of the operation of the system.
1. A condensate drain device comprising:
(a) a metal housing substantially cylindrical in shape having a two-stage central
longitudinal bore, an upper stage wherein the bore is threaded internally and is larger
than a lower stage wherein the bore is threaded internally to accommodate a conduit;
(b) a metal cap shaft externally threaded just below the cap and adapted to be screwed
into the upper stage bore of the housing, the cap shaft having a two-stage central
longitudinal bore wherein an upper stage bore is internally threaded to accommodate
a conduit and is larger than a lower stage bore, the lower stage bore exiting through
a shaft face, the face having cross shaped slots;
(c) a wicking disk, seated in the upper stage bore of the housing, circular in shape
with a thickness up to about 10 mm and having a hole in the center, the disk circumference
being substantially equal to the circumference of the interior of the upper stage
bore of the housing; and
(d) a baffle disk, circular in shape residing on top of the wicking disk, the baffle
disk having a circumference slightly smaller than the circumference of the interior
of the upper stage bore of the housing such that when the cap shaft is screwed into
the upper stage bore of the housing, pressure is applied by the face of the cap shaft
to the baffle disk.
2. The device of Claim 1 wherein the baffle disk applies pressure on the wicking disk
thereby compressing the wicking disk.
3. The device of Claim 1 wherein the wicking disk is polypropylene.
4. The device of Claim 1 wherein the wicking disk is polyester.
5. The device of Claim 1 wherein the baffle disk is metal.
6. The device of Claim 1 wherein the exterior of a lower portion of the cap shaft has
a circumferential notch to accommodate a gasket surrounding the shaft.